EP2870191B1 - Catalysts for the production of cast polyamide, method for producing and using same - Google Patents

Catalysts for the production of cast polyamide, method for producing and using same Download PDF

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Publication number
EP2870191B1
EP2870191B1 EP13727879.2A EP13727879A EP2870191B1 EP 2870191 B1 EP2870191 B1 EP 2870191B1 EP 13727879 A EP13727879 A EP 13727879A EP 2870191 B1 EP2870191 B1 EP 2870191B1
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Prior art keywords
composition according
heteroatoms
lactam
organic acid
substituted
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German (de)
French (fr)
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EP2870191A1 (en
Inventor
Wilhelm Laufer
Serdar Uestuenbas
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Lanxess Deutschland GmbH
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Lanxess Deutschland GmbH
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Priority to SI201331248T priority Critical patent/SI2870191T1/en
Priority to EP13727879.2A priority patent/EP2870191B1/en
Priority to PL13727879T priority patent/PL2870191T3/en
Publication of EP2870191A1 publication Critical patent/EP2870191A1/en
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J31/00Catalysts comprising hydrides, coordination complexes or organic compounds
    • B01J31/02Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides
    • B01J31/12Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides containing organo-metallic compounds or metal hydrides
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G69/00Macromolecular compounds obtained by reactions forming a carboxylic amide link in the main chain of the macromolecule
    • C08G69/02Polyamides derived from amino-carboxylic acids or from polyamines and polycarboxylic acids
    • C08G69/08Polyamides derived from amino-carboxylic acids or from polyamines and polycarboxylic acids derived from amino-carboxylic acids
    • C08G69/14Lactams
    • C08G69/16Preparatory processes
    • C08G69/18Anionic polymerisation
    • C08G69/20Anionic polymerisation characterised by the catalysts used
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J37/00Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
    • B01J37/08Heat treatment
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C63/00Compounds having carboxyl groups bound to a carbon atoms of six-membered aromatic rings
    • C07C63/14Monocyclic dicarboxylic acids
    • C07C63/15Monocyclic dicarboxylic acids all carboxyl groups bound to carbon atoms of the six-membered aromatic ring
    • C07C63/261,4 - Benzenedicarboxylic acid
    • C07C63/28Salts thereof
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07DHETEROCYCLIC COMPOUNDS
    • C07D201/00Preparation, separation, purification or stabilisation of unsubstituted lactams
    • C07D201/14Preparation of salts or adducts of lactams
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G75/00Macromolecular compounds obtained by reactions forming a linkage containing sulfur with or without nitrogen, oxygen, or carbon in the main chain of the macromolecule
    • C08G75/02Polythioethers
    • C08G75/0204Polyarylenethioethers
    • C08G75/025Preparatory processes
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L79/00Compositions of macromolecular compounds obtained by reactions forming in the main chain of the macromolecule a linkage containing nitrogen with or without oxygen or carbon only, not provided for in groups C08L61/00 - C08L77/00
    • C08L79/04Polycondensates having nitrogen-containing heterocyclic rings in the main chain; Polyhydrazides; Polyamide acids or similar polyimide precursors
    • C08L79/08Polyimides; Polyester-imides; Polyamide-imides; Polyamide acids or similar polyimide precursors

Definitions

  • the present invention relates to novel catalysts for the production of cast polyamide, processes for their preparation and their use.
  • Cast polyamides are particularly high molecular weight polyamides.
  • a lactam is poured into a mold together with at least one catalyst and at least one activator and then anionically polymerized in this form.
  • the starting compounds present in the form polymerize generally under the action of heat. The result is a homogeneous material, which exceeds extruded polyamides in terms of crystallinity.
  • Cast polyamides are suitable as thermoplastic materials for the production of complex components. In contrast to many other thermoplastics, they do not need to be melted, but are formed by anionic polymerization of the lactam in a mold at 120 ° to 150 ° C. in just a few minutes. In this case, all known casting methods, such as casting, injection molding, rotary and centrifugal casting, can be applied.
  • Cast polyamides can be sawing, drilling, milling, grinding, welding and printing or painting; In addition to complex molds are made of this polymer, for example, rolls for passenger lifts and semi-finished products, such as tubes, rods and plates for mechanical engineering and the automotive industry.
  • the object of the present invention was therefore to provide new compositions which are suitable as catalysts in the preparation of cast polyamides, and which do not have the disadvantages of the prior art.
  • compositions according to the invention have this property profile.
  • lactamates a) are at least one compound selected from the group of alkali aluminum dilactamates, alkali metal and / or alkaline earth metal lactamates.
  • lactamate in the context of the invention are alkali metal and / or alkaline earth metal lactamates, preferably sodium, potassium and / or magnesium, individually or in a mixture.
  • lactamates are commercially available and are available, for example, from Rhein Chemie Rheinau GmbH.
  • the ester b) is C 1 -C 6 -alkyl ester, preferably methyl, and / or ethyl ester.
  • the heteroatom-substituted organic acid preferably has 1-12 carbon atoms, preferably 4-6 carbon atoms.
  • the salt of an organic acid substituted by heteroatoms, preferably amino groups, b) has 1 to 12 carbon atoms, more preferably 4 to 6 carbon atoms.
  • the heteroatoms are nitrogen, sulfur, phosphorus, preferably nitrogen, particularly preferably amino groups, and / or halides, preferably chlorine and / or bromine.
  • the salt of a heteroatom-substituted organic acid and / or ester of a heteroatom-substituted organic acid b) is particularly preferably aminocapronates and / or aminolaurates, preferably alkali metal and / or alkaline earth metal aminocapronates and / or laurates, particularly preferably sodium , Potassium and / or magnesium aminocapronate.
  • the lactam c) is a compound of the general formula wherein R * represents an alkylene group having 3 to 13 carbon atoms.
  • capro-lactam and / or lauryl lactam are commercially available, e.g. at the Lanxess Germany GmbH.
  • composition according to the invention preferably has components a) and b) in a ratio of 3: 1 to 50: 1, preferably 5: 1 to 40: 1, particularly preferably 9: 1.
  • the content of lactam c), based on constituents a) and b), is preferably 0-99% by weight, particularly preferably 50-85% by weight.
  • Another object of the invention is a process for the preparation of the composition according to the invention in which the lactamate a) by reacting at least one lactam, which lactam c), but may also be different, with alkali or alkaline earth alcoholates in the presence of at least one salt of a heteroatom-substituted organic acid and / or ester of a heteroatom-substituted organic acid b) is prepared by subsequent or simultaneous removal of the resulting alcohol by distillation and then optionally further lactam c) is added.
  • the lactamate a) by reacting at least one lactam, which lactam c), but may also be different, with alkali or alkaline earth alcoholates in the presence of at least one salt of a heteroatom-substituted organic acid and / or ester of a heteroatom-substituted organic acid b) is prepared by subsequent or simultaneous removal of the resulting alcohol by distillation and then optionally further lactam c) is added.
  • the lactamate a) is converted by reaction of lactam, preferably caprolactam, which corresponds to lactam c), but may also be different therefrom, with Na-methoxide in the presence of Na-aminocapronate and / or Na-Aminolaurate b) produced by subsequent or simultaneous removal of the resulting alcohol by distillation and then optionally further lactam c) was added.
  • lactam preferably caprolactam, which corresponds to lactam c
  • Na-methoxide in the presence of Na-aminocapronate and / or Na-Aminolaurate b) produced by subsequent or simultaneous removal of the resulting alcohol by distillation and then optionally further lactam c) was added.
  • the lactamate a) is reacted by reacting at least one caprolactam in excess, which corresponds to lactam c), with Na-methoxide in the presence of Na-aminocaproate and / or Na-aminolaurate b) in subsequent or simultaneous Removal of the resulting alcohol produced by distillation.
  • the aforementioned reactions i. the preparation of the lactamate and the distillation are preferably carried out at temperatures of 80 ° - 130 ° C.
  • the process according to the invention can be carried out both as a batch process and in a continuous process.
  • the salts of a heteroatom-substituted organic acid and / or esters of heteroatom-substituted organic acids before, during and / or after the preparation of the lactamate a) can be added.
  • the process variant in which the salts of a heteroatom-substituted organic acid and / or esters of heteroatom-substituted organic acids are formed "in situ".
  • the in situ preparation of the salts of a heteroatom-substituted organic acid and / or esters of heteroatom-substituted organic acids b) by addition of acids, water and / or alkali and / or alkaline earth metal hydroxides to a) and if necessary c).
  • Particularly preferred is the addition of stoichiometrically required amounts of water to adjust the desired salt concentrations.
  • the lactamate a) is melted at temperatures of 80-120 ° C., optionally together with lactam c), and with at least one salt of a heteroatom-substituted organic acid and / or ester of the heteroatom-substituted organic acid b), preferably with stirring.
  • stirring For stirring, commercially available stirring units, such as preferably stirred tanks or mixers, can be used.
  • compositions obtainable by the aforementioned inventive method are compositions obtainable by the aforementioned inventive method.
  • cast polyamides obtainable by the polymerization of lactams with at least one inventive composition of a) and b) and optionally c) at temperatures of 80-180 ° C, preferably of 120 and 160 ° C, in the presence of activators and optionally further additives and auxiliaries.
  • the preparation is preferably carried out according to the molding process familiar to the person skilled in the art, such as, preferably, injection molding, continuous casting and / or rotational casting.
  • the polymerization of lactams is preferably carried out by adding the inventive composition in the melted at temperatures of 80 - 120 ° C lactam and subsequent addition of a Lactamschmelze with at least one activator and other additives and excipients.
  • the polymerization for producing the cast polyamides is preferably carried out directly in the casting mold.
  • the polymerization is preferably carried out under exclusion of atmospheric moisture z. B. in a vacuum or in an inert atmosphere.
  • isocyanates As activators for the purposes of the invention, isocyanates, isocyanurates, biurets, allophanates, uretdiones and / or carbodiimides may be used as a single compound or in the form of a mixture. Also usable in the context of the invention are activators that are blocked, z. B. with lactams, particularly preferably caprolactam, with phenols, oximes and / or epoxides as well as solvent-containing activators.
  • Suitable solvents are: N-alkylpyrrolidones, preferably, N-methylpyrrolidone and N-ethylpyrrolidone, polyglycols, preferably polyglycol DME 200, dipropylene glycol DME or tetraethylene glycol DME.
  • Isocyanates according to the invention are preferably diisocyanates, more preferably 2,4-tolylene diisocyanate (TDI), 2,6-tolylene diisocyanate, a mixture of 2,4-tolylene diisocyanate and 2,6-tolylene diisocyanate, hexamethylene-1,6-diisocyanate, cyclohexane 1,4-diisocyanate, xylylene diisocyanate, isophorone diisocyanate, 1,5-naphthalene diisocyanate, 4,4'-diphenylmethane diisocyanate, 2,4'-diphenylmethane diisocyanate, 2,2'-diphenylmethane diisocyanate, 4,4'-diphenyldimethylmethane diisocyanate, 1 , 3-phenylene diisocyanate, 1,4-phenylene diisocyanate, dicyclohexylmethane-4,4'-
  • Uretdiones in the context of the invention are reaction products of at least two isocyanates with the formation of dioxodiazetidine bonds:
  • the preparation is known per se to the person skilled in the art.
  • the compounds may, for example, according to the in EP 1 422 223 A1 be prepared described methods.
  • the uretdione may be a dimer, trimer, oligomer or polymer.
  • uretdiones are known per se to the person skilled in the art. Preference is given to uretdiones which are obtained starting from an aliphatic or aromatic isocyanate.
  • the aromatic isocyanates have as R preferably 6 to 20 carbon atoms, more preferably 6 to 15 carbon atoms.
  • Corresponding aromatic monomeric isocyanates may, for example, be selected from the group consisting of 2,4-diisocyanatotoluene, 2,6-diisocyanatotoluene, 1,5-naphthylene diisocyanate, 4,4'-methylene diphenyl diisocyanate, 1,3-bis (3 isocyanato-4-methylphenyl) -2,4-dioxodiazetidine, N, N'-bis (4-methyl-3-isocyanatophenyl) urea and tetramethylxylylene diisocyanate.
  • aromatic isocyanates 2,4-diisocyanatotoluene, 2,6-diisocyanatotoluene and 4,4'-methylene-bis (phenyl diisocyanate) are preferable. Particularly preferred are 2,6-diisocyanatotoluene and 4,4'-methylene-bis (phenyl diisocyanate).
  • the aliphatic isocyanates have as R preferably 6 to 20 carbon atoms, more preferably 6 to 15 carbon atoms.
  • Corresponding aliphatic monomeric isocyanates may for example be selected from the group consisting of isophorone diisocyanate, 1,4-cyclohexyl diisocyanate, 1,1-methylene-bis (4-isocyanatocyclohexane), 1,2-bis (4-isocyanatononyl) -3- heptyl-4-pentylcyclohexane and hexamethylene-1,6-diisocyanate.
  • the use of isophorone diisocyanate and hexamethylene-1,6-diisocyanate is preferred.
  • Allophanates within the meaning of the invention are preferably compounds of the formula (VI) where R 'and R "independently of one another are an alkyl radical having 1 to 20 carbon atoms or an aryl radical having 6 to 20 carbon atoms, and R '"has the meaning of an alkyl radical having 1 to 20 carbon atoms
  • R "OOC-NHR ' monoisocyanates of the general formula R"' - NCO or with diisocyanates general formula OCN-A-NCO accessible
  • R '"or A is preferably an alkyl radical having 1 to 20 carbon atoms or an aryl radical having 6 to 20 carbon atoms
  • R' and R" are independently alkyl radicals having 1 to 20 carbon atoms or aryl radicals with 6 to 20 carbon atoms.
  • Suitable monoisocyanates are any aromatic, aliphatic and cycloaliphatic monoisocyanates containing up to 20 carbon atoms, such as methyl isocyanate, isopropyl isocyanate, n-butyl isocyanate, n-hexyl isocyanate, cyclohexyl isocyanate, stearyl isocyanate, the optionally halogenated phenyl isocyanates, 1-naphthyl isocyanate, which may be chlorinated or fluorinated.
  • o-, and p-tooleyl isocyanates p-isopropylphenyl isocyanate, 2,6-diisopropylphenyl isocyanate and p-toluenesulfonyl diisocyanate.
  • Suitable diisocyanates are any aromatic, aliphatic and cycloaliphatic diisocyanates having 6 to 40 carbon atoms, preferably 6 to 15 carbon atoms, more preferably isophorone diisocyanate, 1,4-cyclohexyl diisocyanate, 1,1-methylene-bis- (isocyanatohexane), 1,2- Bis (4-isocyanatononyl) -3-heptyl-4-pentylcyclohexane, hexamethylene-1,6-diisocyanate, 2,4-diisocyanatotoluene, 2,6-diisocyanatotoluene, 1,5-naphthylene diisocyanate, 4,4'-methylene diphenyl diisocyanate , 1,3-bis (3-isocyanto-4-methylphenyl) -2,4-dioxodiazetidine, N, N'-bis (4-methyl-3-isocyanato
  • the allophanates which are particularly preferred in the context of the present invention are compounds of the formula (VII) wherein R 4 and R 6 may be the same or different within the molecule and C 1 -C 6 alkyl, preferably - (CH 2 ) 6 -, and R 5 is C 1 -C 6 alkyl.
  • carbodiimides of the formula (VIII) including the corresponding oligomers and / or polymers, with polymeric carbodiimides being preferred.
  • the compounds of the formula (VIII) are commercially available, for example from Rhein Chemie Rheinau GmbH, or can be prepared by the processes familiar to the person skilled in the art, as described, for example, in US Pat DE-A-11 30 594 or US-A 2,840,589 or by the condensation of diisocyanates with elimination of carbon dioxide at elevated temperatures, for example at 40 ° C to 200 ° C, in the presence of catalysts.
  • catalysts preferably strong bases or phosphorus compounds have proven. Preference is given to using phospholene oxides, phospholidines or phospholine oxides and the corresponding sulfides.
  • tertiary amines basic metal compounds, carboxylic acid metal salts and non-basic organometallic compounds can be used.
  • Blocked activators preferably with lactams, particularly preferably caprolactam, or activators blocked with phenols, oximes and / or epoxides
  • lactams particularly preferably caprolactam
  • activators blocked with phenols, oximes and / or epoxides can be prepared, for example, by reacting at least one compound of the formulas (I) to (VIII) with at least one lactam, Caprolactam, phenol, oxime and / or epoxide at temperatures of 80 to 100 ° C according to the methods known in the art.
  • the following proportions are preferably used in one embodiment of the invention, based on lactam: 0.1 to 3 wt.%, Preferably 0.2 to 1.5 wt.% Of the inventive composition and 0.1 to 2 wt.%, Preferably 0.5 to 1 wt.% Of activator.
  • lactam preferably caprolactam 0.1 to 3 wt.% Of the inventive composition containing sodium lactamate a) as preferably 18-20 wt.%
  • the mixture for the production of cast polyamides additionally contains at least one further additive and adjuvant, selected from fillers and / or reinforcing materials, polymers and / or further additives.
  • Fillers and / or reinforcing agents in the context of the invention are organic or inorganic fillers and / or reinforcing materials.
  • inorganic fillers in particular kaolin, chalk, wollastonite, talc, calcium carbonate, silicates, titanium dioxide, zinc oxide, graphite, graphenes, glass particles (eg glass spheres), nanoscale fillers (such as carbon nanotubes carbonanotubes), carbon black, phyllosilicates, nanoscale phyllosilicates , nanoscale alumina (Al 2 O 3 ), nanoscale titania (TiO 2 ), and / or nanoscale silica (SiO 2 ).
  • the fillers and / or reinforcing materials are usually selected from the group comprising minerals in customary for thermoplastic applications grain size, in particular kaolin, chalk, wollastonite or talc, carbon or glass fibers, preferably ground glass fibers, particularly preferably glass and carbon fibers.
  • one or more fibrous materials selected from known inorganic reinforcing fibers, in particular boron fibers, glass fibers, carbon fibers, silica fibers, ceramic fibers and basalt fibers; organic reinforcing fibers, especially aramid fibers, polyester fibers, nylon fibers, polyethylene fibers; and natural fibers, especially wood fibers, flax fibers, hemp fibers and sisal fibers.
  • organic reinforcing fibers especially aramid fibers, polyester fibers, nylon fibers, polyethylene fibers
  • natural fibers especially wood fibers, flax fibers, hemp fibers and sisal fibers.
  • glass fibers in particular chopped glass fibers, carbon fibers, aramid fibers, boron fibers, metal fibers and / or potassium titanate fibers.
  • Glass fibers and / or glass particles, in particular glass beads, are particularly preferably selected as fillers and / or reinforcing materials.
  • the amount of fillers and / or reinforcing substances to be used is preferably from 30 to 90% by weight, in particular from 30 to 80% by weight, preferably from 30 to 50% by weight, more preferably from 50 to 90% by weight.
  • Polymers in the context of the invention are: polystyrene, styrene copolymers, in particular styrene-acrylonitrile copolymers (SAN), acrylonitrile-butadiene-styrene copolymers (ABS) or styrene-butadiene copolymers (SB), polyphenylene oxide ethers, polyolefins, in particular polyethylene (HTPE ( high-temperature polyethylene), LTPE (low-temperature polyethylene), polypropylene or polybutene-1, polytetrafluoroethylene, polyesters, in particular polyethylene terephthalate (PET), polyamides, polyethers, in particular polyethylene glycol (PEG), polypropylene glycol or polyethersulfones (PESU or PES)
  • Polymers made from vinyl groups contain monomers, in particular polyvinyl chloride, polyvinylidene chlorides, polystyrene, impact-modified polysty
  • the polymer to be used may contain groups which are suitable for forming block and / or graft copolymers with the polymer formed from the monomers.
  • groups are epoxy, amine, carboxyl anhydride, oxazoline, carbodiimide, urethane, isocyanate and lactam groups.
  • Polymers with carbodiimide groups are used when no carbodiimide is used as activator.
  • Optionally contained polymer is preferably contained in an amount of 0 to 40 wt .-%, preferably from 0 to 20 wt .-%, particularly preferably in an amount of 0 to 10 wt .-%.
  • the composition according to the invention contains further additives.
  • the additives are preferably used in an amount of from 0 to 5% by weight, particularly preferably from 0 to 4% by weight, very particularly preferably from 0 to 3.5% by weight.
  • Stabilizers in particular copper salts, dyes, antistatic agents, fillers, stabilizers, surface improvers, siccatives, mold release agents, release agents, antioxidants, light stabilizers, PVC stabilizers, lubricants, polyols, flame retardants, blowing agents, impact modifiers and / or nucleating agents may preferably be added as additives ,
  • Particularly suitable impact modifiers are polydiene polymers, preferably polybutadiene, polyisoprene, containing anhydride and / or epoxy groups.
  • the polydiene polymer has a glass transition temperature below 0 ° C, preferably below -10 ° C, more preferably below -20 ° C.
  • the polydiene polymer can be based on a polydiene copolymer with polyacrylates, polyethylene acrylates and / or polysiloxanes and prepared by the usual methods, preferably by emulsion polymerization, suspension polymerization, solution polymerization, gas phase polymerization.
  • additive polyol to improve the impact resistance.
  • additive polyol e.g. available from Rhein Chemie Rheinau GmbH under the name Addonyl® 8073.
  • polyoltriamines suitable for improving the low-temperature impact strength.
  • a suitable product is Addonyl® 8112.
  • the polyols are used in the concentration range 1-20 wt .-%.
  • fillers and / or reinforcing materials and other additives can be carried out before or together with the addition of catalyst and / or activator.
  • the polymerization for the production of cast polyamides may be carried out by a suitable molding process, preferably injection molding, casting, rotational molding.
  • Injection molding, stand casting, rotational molding process are familiar to those skilled in the process.
  • Another object of the present invention is the use of the composition of the invention as a catalyst for the production of cast polyamide.
  • composition according to the invention for the production of rolls, preferably for passenger lifts and semi-finished products, preferably containers, gears, tubes, rods and plates for mechanical engineering and the automotive industry is a further subject of the invention.
  • Caprolactam dry (EP> 69 ° C) from the company Lanxess Germany GmbH Activator, a hexamethylene-1,6-diisocyanate (HDI) biuret, 70% in N-ethylpyrrolidone, commercially available from Rhein Chemie Rheinau GmbH, Inventive composition as catalyst (A) with about 18% sodium caprolactamate and 2.0% sodium aminocapronate in caprolactam.
  • HDI hexamethylene-1,6-diisocyanate
  • Flask A was charged with 196.8 g of caprolactam and 3.2 g of activator, flask B1 / 2 with 192 g of caprolactam and 8 g of catalyst (A) and (B), respectively.
  • the melts from flask A and flask B1 / 2 were conditioned at 110-130 ° C ( ⁇ 2 ° C) in an oil bath under vacuum ( ⁇ 15 mbar) for 20 minutes.
  • the mold temperature (beaker) was 160 ° C.
  • the polymerization time was generally 10 to 20 minutes.
  • the turbidity tests were carried out in a drying oven at 85 ° C. after a period of 3 hours. The assessment was done visually.
  • the blends of the prior art have i.d.R. Pot lives of ⁇ 300s, resulting in inhomogeneities and a low crystallinity of the cast polyamide.
  • the melts containing the catalyst polymerize already in the template and thus clog the filter upstream of the mold.
  • the examples show that the catalyst according to the invention has pot lives of well over 300s. Moreover, the compositions according to the invention do not tarnish.

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Description

Die vorliegenden Erfindung betrifft neue Katalysatoren für die Herstellung von Gusspolyamid, Verfahren zu deren Herstellung und deren Verwendung.The present invention relates to novel catalysts for the production of cast polyamide, processes for their preparation and their use.

Gusspolyamide sind besonders hochmolekulare Polyamide. Bei der Herstellung von Gusspolyamiden wird ein Lactam zusammen mit mindestens einem Katalysator und mindestens einem Aktivator in eine Form gegossen und dann in dieser Form anionisch polymerisiert. Die in der Form vorliegenden Ausgangsverbindungen polymerisieren dabei im Allgemeinen unter Einwirkung von Wärme. Dabei entsteht ein homogener Werkstoff, welcher extrudierte Polyamide im Hinblick auf die Kristallinität übertrifft.Cast polyamides are particularly high molecular weight polyamides. In the production of cast polyamides, a lactam is poured into a mold together with at least one catalyst and at least one activator and then anionically polymerized in this form. The starting compounds present in the form polymerize generally under the action of heat. The result is a homogeneous material, which exceeds extruded polyamides in terms of crystallinity.

Gusspolyamide sind als thermoplastische Kunststoffe für die Fertigung komplexer Bauteile geeignet. Sie müssen im Gegensatz zu vielen anderen Thermoplasten nicht aufgeschmolzen werden, sondern entstehen durch anionische Polymerisation des Lactams in einer Form bei 120° bis 150°C bereits in wenigen Minuten. Dabei können alle bekannten Gießverfahren, wie Standguss, Spritzguss, Rotations- und Schleuderguss, angewendet werden. Als Endprodukt erhält man jeweils Formteile aus einem hochmolekularen, kristallinen Polyamid, das sich durch ein niedriges Gewicht, eine hohe mechanische Belastbarkeit, sehr gute Gleiteigenschaften und eine hervorragende Chemikalienbeständigkeit auszeichnet und das - da die Formen nicht unter Druck gefüllt werden - nur geringe innere Spannungen aufweist. Gusspolyamide lassen sich Sägen, Bohren, Fräsen, Schleifen, Verschweißen und Bedrucken oder Lackieren; neben komplexen Hohlformen werden aus diesem Polymer beispielsweise auch Rollen für Personenaufzüge und Halbzeuge, wie zum Beispiel Rohre, Stäbe und Platten für den Maschinenbau und die Automobilindustrie, gefertigt.Cast polyamides are suitable as thermoplastic materials for the production of complex components. In contrast to many other thermoplastics, they do not need to be melted, but are formed by anionic polymerization of the lactam in a mold at 120 ° to 150 ° C. in just a few minutes. In this case, all known casting methods, such as casting, injection molding, rotary and centrifugal casting, can be applied. The final product obtained in each case molded parts from a high molecular weight, crystalline polyamide, which is characterized by a low weight, high mechanical strength, very good sliding properties and excellent chemical resistance and - since the molds are not filled under pressure - has only low internal stresses , Cast polyamides can be sawing, drilling, milling, grinding, welding and printing or painting; In addition to complex molds are made of this polymer, for example, rolls for passenger lifts and semi-finished products, such as tubes, rods and plates for mechanical engineering and the automotive industry.

Die Herstellung von Gusspolyamidteilen, ausgehend von niedrig viskosen Lactamschmelzen und einem Katalysator sowie einem Aktivator, durch die sogenannte aktivierte anionische Polymerisation, ist an sich bekannt. Zu diesem Zweck werden üblicherweise zwei Mischungen aus Katalysator und Lactam bzw. Aktivator und Lactam in Form einer flüssigen Schmelze miteinander vermischt und anschließend in der Gussform polymerisiert, siehe EP-A-2447302 . Aus US-A 3 663 670 ist ein Verfahren zur Polymerisation von Lactamen bekannt, wonach Lactam und Natriumhydrid in Gegenwart von Kaliumstearat umgesetzt und anschließend diese Mischung mit weiterem Lactam umgesetzt wird. Nachteilig bei den derzeitigen Katalysatoren für Gusspolyamide ist jedoch die zu hohe und nicht konstante Reaktivität. Dies führt zu schlechteren Produkteigenschaften, wie z. B. geringer Kristallinität, und macht das Procedere vor allem bei großen Gussteilen unwirtschaftlich.The production of cast polyamide parts, starting from low-viscosity lactam melts and a catalyst and an activator, by the so-called activated anionic polymerization, is known per se. For this purpose, usually two mixtures of catalyst and lactam or activator and lactam in the form of a liquid melt are mixed together and then polymerized in the mold, see EP-A-2447302 , Out US Pat. No. 3,663,670 For example, a process for the polymerization of lactams is known, after which lactam and sodium hydride are reacted in the presence of potassium stearate and then this mixture is reacted with further lactam. A disadvantage of the current catalysts for cast polyamides, however, is the too high and not constant reactivity. This leads to poorer product properties, such. B. low crystallinity, and makes the procedure especially for large castings uneconomical.

Die Aufgabe der vorliegenden Erfindung bestand somit darin, neue Zusammensetzungen bereitzustellen, die sich als Katalysatoren bei der Herstellung von Gusspolyamiden eignen, und die die Nachteile des Standes der Technik nicht aufweisen.The object of the present invention was therefore to provide new compositions which are suitable as catalysts in the preparation of cast polyamides, and which do not have the disadvantages of the prior art.

Überraschenderweise wurde nun gefunden, dass die erfindungsgemäßen Zusammensetzungen dieses Eigenschaftsprofil aufweisen.Surprisingly, it has now been found that the compositions according to the invention have this property profile.

Gegenstand der vorliegenden Erfindung sind somit Zusammensetzungen enthaltend

  1. a) mindestens ein Lactamat und
  2. b) mindestens ein Salz einer mit Heteroatomen substituierten organischen Säure und/oder Ester einer mit Heteroatomen substituierten organischen Säure und gegebenenfalls
  3. c) mindestens ein Lactam.
The subject of the present invention are thus compositions containing
  1. a) at least one lactamate and
  2. b) at least one salt of a heteroatom-substituted organic acid and / or ester of a heteroatom-substituted organic acid and optionally
  3. c) at least one lactam.

In einer bevorzugten Ausführungsform der Erfindung handelt es sich bei Lactamaten a) um mindestens eine Verbindung, ausgewählt aus der Gruppe der Alkali-Alumo-Dilactamate, Alkali- und/oder Erdalkalilactamate.In a preferred embodiment of the invention, lactamates a) are at least one compound selected from the group of alkali aluminum dilactamates, alkali metal and / or alkaline earth metal lactamates.

Bevorzugt als Lactamat im Sinne der Erfindung sind Alkali- und/oder Erdalkalilactamate, bevorzugt Natrium, Kalium und/oder Magnesium, einzeln oder im Gemisch.Preferred as lactamate in the context of the invention are alkali metal and / or alkaline earth metal lactamates, preferably sodium, potassium and / or magnesium, individually or in a mixture.

Die vorgenannten Lactamate sind handelsüblich und sind beispielsweise bei der Firma Rhein Chemie Rheinau GmbH erhältlich.The aforementioned lactamates are commercially available and are available, for example, from Rhein Chemie Rheinau GmbH.

In einer bevorzugten Ausführungsform der Erfindung handelt es sich bei dem Ester b) um C1-C6 - Alkylester, bevorzugt Methyl-, und/oder Ethylester. Die mit Heteroatomen substituierte organische Säure hat dabei vorzugsweise 1-12 Kohlenstoffatome, bevorzugt 4-6 Kohlenstoffatome.In a preferred embodiment of the invention, the ester b) is C 1 -C 6 -alkyl ester, preferably methyl, and / or ethyl ester. The heteroatom-substituted organic acid preferably has 1-12 carbon atoms, preferably 4-6 carbon atoms.

In einer bevorzugten Ausführungsform der Erfindung hat das Salz einer mit Heteroatomen, vorzugsweise Aminogruppen, substituierten organischen Säure b) 1 - 12 -Kohlenstoffatome, besonders bevorzugt 4 - 6 Kohlenstoffatome.In a preferred embodiment of the invention, the salt of an organic acid substituted by heteroatoms, preferably amino groups, b) has 1 to 12 carbon atoms, more preferably 4 to 6 carbon atoms.

In einer besonders bevorzugten Ausführungsform der Erfindung handelt es sich bei den Heteroatomen um Stickstoff, Schwefel, Phosphor, vorzugsweise Stickstoff, besonders bevorzugt Aminogruppen, und/oder um Halogenide, vorzugsweise Chlor und/oder Brom.In a particularly preferred embodiment of the invention, the heteroatoms are nitrogen, sulfur, phosphorus, preferably nitrogen, particularly preferably amino groups, and / or halides, preferably chlorine and / or bromine.

Besonders bevorzugt handelt es sich bei dem Salz einer mit Heteroatomen substituierten organischen Säure und/oder Ester einer mit Heteroatomen substituierten organischen Säure b) um Aminocapronate und/oder Aminolaurate, bevorzugt Alkali- und/ oder Erdalkaliaminocapronate und/oder -Laurate, besonders bevorzugt Natrium-, Kalium- und/oder Magnesium-Aminocapronat.The salt of a heteroatom-substituted organic acid and / or ester of a heteroatom-substituted organic acid b) is particularly preferably aminocapronates and / or aminolaurates, preferably alkali metal and / or alkaline earth metal aminocapronates and / or laurates, particularly preferably sodium , Potassium and / or magnesium aminocapronate.

In einer bevorzugten Ausführungsform der Erfindung handelt es sich bei dem Lactam c) um eine Verbindung der allgemeinen Formel

Figure imgb0001
wobei R* eine Alkylengruppe mit 3 bis 13 Kohlenstoffatomen darstellt.In a preferred embodiment of the invention, the lactam c) is a compound of the general formula
Figure imgb0001
wherein R * represents an alkylene group having 3 to 13 carbon atoms.

Bevorzugt sind dabei Capro-Lactam und/oder Laurin-Lactam. Diese sind kommerziell erhältlich, z.B. bei der Lanxess Deutschland GmbH.Preference is given to capro-lactam and / or lauryl lactam. These are commercially available, e.g. at the Lanxess Germany GmbH.

Die erfindungsgemäße Zusammensetzung weist dabei vorzugsweise die Bestandteile a) und b) im Verhältnis 3:1 bis 50: 1, bevorzugt 5:1 bis 40: 1, besonders bevorzugt 9:1 auf.The composition according to the invention preferably has components a) and b) in a ratio of 3: 1 to 50: 1, preferably 5: 1 to 40: 1, particularly preferably 9: 1.

Der Anteil an Lactam c), bezogen auf die Bestandteile a) und b) beträgt vorzugsweise 0 - 99 Gew.%, besonders bevorzugt 50 - 85 Gew.%.The content of lactam c), based on constituents a) and b), is preferably 0-99% by weight, particularly preferably 50-85% by weight.

Ein weiterer Gegenstand der Erfindung ist ein Verfahren zur Herstellung der erfindungsgemäßen Zusammensetzung bei dem das Lactamat a) durch Umsetzung von mindestens einem Lactam, welches Lactam c) entspricht, aber auch von diesem verschieden sein kann, mit Alkali- oder Erdalkali-Alkoholaten in Gegenwart von mindestens einem Salz einer mit Heteroatomen substituierten organischen Säure und/oder Ester einer mit Heteroatomen substituierten organischer Säure b) bei anschließender oder gleichzeitiger Entfernung des entstehenden Alkohols durch Destillation hergestellt und anschließend gegebenenfalls weiteres Lactam c) zugesetzt wird.Another object of the invention is a process for the preparation of the composition according to the invention in which the lactamate a) by reacting at least one lactam, which lactam c), but may also be different, with alkali or alkaline earth alcoholates in the presence of at least one salt of a heteroatom-substituted organic acid and / or ester of a heteroatom-substituted organic acid b) is prepared by subsequent or simultaneous removal of the resulting alcohol by distillation and then optionally further lactam c) is added.

In einer bevorzugten Ausführungsform des erfindungsgemäßen Verfahrens wird das Lactamat a) durch Umsetzung von Lactam, bevorzugt Caprolactam, welches Lactam c) entspricht, aber auch von diesem verschieden sein kann, mit Na-Methanolat in Gegenwart von Na-Aminocapronat und/oder Na-Aminolaurat b) bei anschließender oder gleichzeitiger Entfernung des entstehenden Alkohols durch Destillation hergestellt und anschließend gegebenenfalls weiteres Lactam c) zugesetzt.In a preferred embodiment of the process according to the invention, the lactamate a) is converted by reaction of lactam, preferably caprolactam, which corresponds to lactam c), but may also be different therefrom, with Na-methoxide in the presence of Na-aminocapronate and / or Na-Aminolaurate b) produced by subsequent or simultaneous removal of the resulting alcohol by distillation and then optionally further lactam c) was added.

In einer weiteren bevorzugten Ausführungsform des erfindungsgemäßen Verfahrens wird das Lactamat a) durch Umsetzung von mindestens einem Caprolactam im Überschuss, welches Lactam c) entspricht, mit Na-Methanolat in Gegenwart von Na-Aminocapronat und/oder Na-Aminolaurat b) bei anschließender oder gleichzeitiger Entfernung des entstehenden Alkohols durch Destillation hergestellt.In a further preferred embodiment of the process according to the invention, the lactamate a) is reacted by reacting at least one caprolactam in excess, which corresponds to lactam c), with Na-methoxide in the presence of Na-aminocaproate and / or Na-aminolaurate b) in subsequent or simultaneous Removal of the resulting alcohol produced by distillation.

Die vorgenannten Umsetzungen, d.h. die Herstellung des Lactamats sowie die Destillation, werden vorzugsweise bei Temperaturen von 80°- 130°C durchgeführt.The aforementioned reactions, i. the preparation of the lactamate and the distillation are preferably carried out at temperatures of 80 ° - 130 ° C.

Das erfindungsgemäße Verfahren kann sowohl als Batch- als auch in einem Konti-Prozeß erfolgen. Dabei können die Salze einer mit Heteroatomen substituierten organischen Säure und/oder Ester einer mit Heteroatomen substituierten organischer Säuren vor, während und/oder auch nach der Herstellung des Lactamats a) zugegeben werden.The process according to the invention can be carried out both as a batch process and in a continuous process. In this case, the salts of a heteroatom-substituted organic acid and / or esters of heteroatom-substituted organic acids before, during and / or after the preparation of the lactamate a) can be added.

Ebenfalls bevorzugt ist die Verfahrensvariante, bei der die Salze einer mit Heteroatomen substituierten organischen Säure und/oder Ester der mit Heteroatomen substituierten organischen Säuren "in situ" entstehen. In einer bevorzugten Ausführungsform der Erfindung erfolgt die in situ Herstellung der Salze einer mit Heteroatomen substituierten organischen Säure und/oder Ester der mit Heteroatomen substituierten organischen Säuren b) durch Zugabe von Säuren, Wasser und/oder Alkali- und/oder Erdalkalihydroxiden zu a) und gegebenenfalls c). Besonders bevorzugt ist dabei die Zugabe von stöchiometrisch benötigten Wassermengen zur Einstellung der gewünschten Salz-Konzentrationen.Likewise preferred is the process variant in which the salts of a heteroatom-substituted organic acid and / or esters of heteroatom-substituted organic acids are formed "in situ". In a preferred embodiment of the invention, the in situ preparation of the salts of a heteroatom-substituted organic acid and / or esters of heteroatom-substituted organic acids b) by addition of acids, water and / or alkali and / or alkaline earth metal hydroxides to a) and if necessary c). Particularly preferred is the addition of stoichiometrically required amounts of water to adjust the desired salt concentrations.

In einer weiteren Ausführungsform der Erfindung wird das Lactamat a) bei Temperaturen von 80 - 120°C gegebenenfalls zusammen mit Lactam c) aufgeschmolzen und mit mindestens einem Salz einer mit Heteroatomen substituierten organischen Säure und/oder Ester der mit Heteroatomen substituierten organischen Säure b), vorzugsweise unter Rühren, versetzt.In a further embodiment of the invention, the lactamate a) is melted at temperatures of 80-120 ° C., optionally together with lactam c), and with at least one salt of a heteroatom-substituted organic acid and / or ester of the heteroatom-substituted organic acid b), preferably with stirring.

Für das Rühren können handelsüblich Rühraggregate, wie vorzugsweise Rührkessel oder Mischer, eingesetzt werden.For stirring, commercially available stirring units, such as preferably stirred tanks or mixers, can be used.

Ein weiterer Gegenstand der Erfindung sind Zusammensetzungen, erhältlich nach den vorgenannten erfindungsgemäßen Verfahren. In Bezug auf diesen Gegenstand der Erfindung wird auf die obigen Ausführungen, inklusive aller bevorzugten Ausführungsformen verwiesen.Another object of the invention are compositions obtainable by the aforementioned inventive method. With respect to this subject matter of the invention, reference is made to the above statements, including all preferred embodiments.

Ebenso Gegenstand der Erfindung sind Gusspolyamide, erhältlich durch die Polymerisation von Lactamen mit mindestens einer erfindungsgemäßen Zusammensetzung aus a) und b) und gegebenenfalls c) bei Temperaturen von 80 - 180°C, vorzugsweise von 120 und 160°C, in Anwesenheit von Aktivatoren und gegebenenfalls weiteren Zusatz- und Hilfsstoffen.Likewise subject of the invention are cast polyamides, obtainable by the polymerization of lactams with at least one inventive composition of a) and b) and optionally c) at temperatures of 80-180 ° C, preferably of 120 and 160 ° C, in the presence of activators and optionally further additives and auxiliaries.

Die Herstellung erfolgt vorzugsweise nach den dem Fachmann geläufigen Formgebungsverfahren, wie vorzugsweise Spritzguss-, Standguss- und/oder Rotationsguss.The preparation is preferably carried out according to the molding process familiar to the person skilled in the art, such as, preferably, injection molding, continuous casting and / or rotational casting.

Die Polymerisation von Lactamen erfolgt vorzugsweise durch Zugabe der erfindungsgemäßen Zusammensetzung in das bei Temperaturen von 80 - 120°C aufgeschmolzene Lactam und anschließender Zugabe einer Lactamschmelze mit mindestens einem Aktivator und weiteren Zusatz- und Hilfsstoffen.The polymerization of lactams is preferably carried out by adding the inventive composition in the melted at temperatures of 80 - 120 ° C lactam and subsequent addition of a Lactamschmelze with at least one activator and other additives and excipients.

Dabei erfolgt die Polymerisation zur Herstellung der Gusspolyamide vorzugsweise direkt in der Gießform.The polymerization for producing the cast polyamides is preferably carried out directly in the casting mold.

Die Polymerisation erfolgt vorzugsweise unter Ausschluss von Luftfeuchtigkeit z. B. im Vakuum oder in inerter Atmosphäre.The polymerization is preferably carried out under exclusion of atmospheric moisture z. B. in a vacuum or in an inert atmosphere.

Als Aktivatoren im Sinne der Erfindung können Isocyanate, Isocyanurate, Biurete, Allophanate, Uretdione und/oder Carbodiimide als Einzelverbindung oder in Form einer Mischung eingesetzt werden. Ebenfalls einsetzbar im Sinne der Erfindung sind Aktivatoren, die geblockt sind, z. B. mit Lactamen, besonders bevorzugt Caprolactam, mit Phenolen, Oximen und/oder Epoxiden ebenso wie lösemittelhaltige Aktivatoren. Als Lösemittel eignen sich: N-Alkylpyrrolidone, vorzugsweise, N-Methylpyrrolidon und N-Ethylpyrrolidon, Polyglycole,vorzugsweise Polyglycol DME 200, Dipropylenglycol DME oder Tetraethylenglykol DME.As activators for the purposes of the invention, isocyanates, isocyanurates, biurets, allophanates, uretdiones and / or carbodiimides may be used as a single compound or in the form of a mixture. Also usable in the context of the invention are activators that are blocked, z. B. with lactams, particularly preferably caprolactam, with phenols, oximes and / or epoxides as well as solvent-containing activators. Suitable solvents are: N-alkylpyrrolidones, preferably, N-methylpyrrolidone and N-ethylpyrrolidone, polyglycols, preferably polyglycol DME 200, dipropylene glycol DME or tetraethylene glycol DME.

Isocyanate im Sinne der Erfindung sind vorzugsweise Diisocyanate, besonders bevorzugt 2,4-Toluylendiisocyanat (TDI), 2,6-Toluylendiisocyanat, ein Gemisch aus 2,4-Toluylendiisocyanat und 2,6-Toluylendiisocyanat, Hexamethylen-1,6-diisocyanat, Cyclohexan-1,4-diisocyanat, Xylylendiisocyanat, Isophorondiisocyanat, 1,5-Naphthalindiisocyanat, 4,4'-Diphenylmethandiisocyanat, 2,4'-Diphenyl-methandiisocyanat, 2,2'-Diphenylmethandiisocyanat, 4,4'-Diphenyldimethyl-methandiisocyanat, 1,3-Phenylen-diisocyanat, 1,4-Phenylendiisocyanat, Dicyclohexylmethan-4,4'-diisocyanat, Dicyclohexylmethan-2,4'-diisocyanat, Dicyclohexylmethan-2,2'-diisocyanat, Methylcyclohexan-diisocyanat, Tetramethylxylylendiisocyanat, 2,6-Diisopropylphenylen-isocyanat und deren Gemische. Besonders bevorzugt ist Hexamethylen-1,6-diisocyanat. Die vorgenannten Verbindungen sind handelsüblich und sind beispielsweise bei der Firma Bayer MaterialScience AG erhältlich.Isocyanates according to the invention are preferably diisocyanates, more preferably 2,4-tolylene diisocyanate (TDI), 2,6-tolylene diisocyanate, a mixture of 2,4-tolylene diisocyanate and 2,6-tolylene diisocyanate, hexamethylene-1,6-diisocyanate, cyclohexane 1,4-diisocyanate, xylylene diisocyanate, isophorone diisocyanate, 1,5-naphthalene diisocyanate, 4,4'-diphenylmethane diisocyanate, 2,4'-diphenylmethane diisocyanate, 2,2'-diphenylmethane diisocyanate, 4,4'-diphenyldimethylmethane diisocyanate, 1 , 3-phenylene diisocyanate, 1,4-phenylene diisocyanate, dicyclohexylmethane-4,4'-diisocyanate, dicyclohexylmethane-2,4'-diisocyanate, dicyclohexylmethane-2,2'-diisocyanate, methylcyclohexane diisocyanate, tetramethylxylylene diisocyanate, 2,6- Diisopropylphenylene isocyanate and mixtures thereof. Particularly preferred is hexamethylene-1,6-diisocyanate. The abovementioned compounds are commercially available and are obtainable, for example, from Bayer MaterialScience AG.

Isocyanurate im Sinne der Erfindung sind vorzugsweise Verbindungen der Formel (I)

Figure imgb0002

  • mit R1, R2 und R3 jeweils unabhängig voneinander -(CH2)m-N=C=O oder-(CH2)q-[(C6H3)(Me/Et)3(N=C=O)] sind, und m = 1 - 12, q = 0 - 6 und Me für Methyl und Et für Ethyl steht, wobei
  • R1, R2 und R3 vorzugsweise gleich sind.
Isocyanurates in the context of the invention are preferably compounds of the formula (I)
Figure imgb0002
  • with R 1 , R 2 and R 3 each independently of one another - (CH 2 ) m -N = C = O or - (CH 2 ) q - [(C 6 H 3 ) (Me / Et) 3 (N = C = O)], and m = 1-12, q = 0-6 and Me is methyl and Et is ethyl, wherein
  • R 1 , R 2 and R 3 are preferably the same.

Dabei sind die folgenden Verbindungen der Formel (II)

Figure imgb0003
und der Formel (III)
Figure imgb0004
bevorzugt.The following compounds of the formula (II)
Figure imgb0003
and the formula (III)
Figure imgb0004
prefers.

Die vorgenannten Verbindungen sind handelsüblich und sind beispielsweise bei der Firma Bayer MaterialScience AG erhältlich.The abovementioned compounds are commercially available and are obtainable, for example, from Bayer MaterialScience AG.

Biurete im Sinne der Erfindung sind vorzugsweise Verbindungen der Formel (IV)

Figure imgb0005

  • mit RIV, RV und RVI jeweils unabhängig voneinander -(CH2)p-N=C=O, mit p = 1 - 12, wobei
  • RIV , RV und RVI vorzugsweise gleich sind.
Biurets within the meaning of the invention are preferably compounds of the formula (IV)
Figure imgb0005
  • with R IV , R V and R VI each independently of one another - (CH 2 ) p -N = C = O, with p = 1-12, where
  • R IV , R V and R VI are preferably the same.

In einer besonders bevorzugten Ausführungsform der Erfindung handelt es sich bei dem Biuret um eine Verbindung der Formel (V), d.h. einem Biuret der Formel (IV) mit RIV, RV und RVI = -(CH2)p-N=C=O und p = 6

Figure imgb0006
In a particularly preferred embodiment of the invention, the biuret is a compound of the formula (V), ie a biuret of the formula (IV) where R IV , R V and R VI = - (CH 2 ) p -N = C = O and p = 6
Figure imgb0006

Die vorgenannten Verbindungen sind handelsüblich und sind beispielsweise bei der Firma Bayer MaterialScience AG erhältlich.The abovementioned compounds are commercially available and are obtainable, for example, from Bayer MaterialScience AG.

Uretdione im Sinne der Erfindung sind Umsetzungsprodukte von mindestens zwei Isocyanaten unter der Ausbildung von Dioxodiazetidin-Bindungen:

Figure imgb0007
Uretdiones in the context of the invention are reaction products of at least two isocyanates with the formation of dioxodiazetidine bonds:
Figure imgb0007

Die Herstellung ist dem Fachmann an sich bekannt. Die Verbindungen können beispielsweise gemäß der in EP 1 422 223 A1 beschriebenen Verfahren hergestellt werden.The preparation is known per se to the person skilled in the art. The compounds may, for example, according to the in EP 1 422 223 A1 be prepared described methods.

Das Uretdion kann ein Dimer, Trimer, Oligomer oder Polymer sein.The uretdione may be a dimer, trimer, oligomer or polymer.

Geeignete Beispiele für Uretdione sind dem Fachmann an sich bekannt. Bevorzugt sind Uretdione, die ausgehend von einem aliphatischen oder aromatischen Isocyanat erhalten werden. Die aromatischen Isocyanate weisen als R vorzugsweise 6 bis 20 Kohlenstoffatome, besonders bevorzugt 6 bis 15 Kohlenstoffatome, auf. Entsprechende aromatische monomere Isocyanate können beispielsweise ausgewählt werden aus der Gruppe, bestehend aus 2,4-Diisocyanatotoluol, 2,6-Diisocyanatotoluol, 1,5-Naphthylendiisocyanat, 4,4'-Methylen-diphenyldiisocyanat, 1,3-Bis-(3-isocyanato-4-methylphenyl)-2,4-dioxodiazetidin, N,N'-Bis-(4-methyl-3-isocyanatophenyl)-Harnstoff und Tetramethylxylylendiisocyanat. Von diesen aromatischen Isocyanaten sind 2,4-Diisocyanatotoluol, 2,6-Diisocyanatotoluol und 4,4'-Methylen-bis(phenyldiisocyanat) bevorzugt. Insbesondere bevorzugt sind 2,6-Diisocyanatotoluol und 4,4'-Methylen-bis(phenyldiisocyanat).Suitable examples of uretdiones are known per se to the person skilled in the art. Preference is given to uretdiones which are obtained starting from an aliphatic or aromatic isocyanate. The aromatic isocyanates have as R preferably 6 to 20 carbon atoms, more preferably 6 to 15 carbon atoms. Corresponding aromatic monomeric isocyanates may, for example, be selected from the group consisting of 2,4-diisocyanatotoluene, 2,6-diisocyanatotoluene, 1,5-naphthylene diisocyanate, 4,4'-methylene diphenyl diisocyanate, 1,3-bis (3 isocyanato-4-methylphenyl) -2,4-dioxodiazetidine, N, N'-bis (4-methyl-3-isocyanatophenyl) urea and tetramethylxylylene diisocyanate. Of these aromatic isocyanates, 2,4-diisocyanatotoluene, 2,6-diisocyanatotoluene and 4,4'-methylene-bis (phenyl diisocyanate) are preferable. Particularly preferred are 2,6-diisocyanatotoluene and 4,4'-methylene-bis (phenyl diisocyanate).

Die aliphatischen Isocyanate weisen als R vorzugsweise 6 bis 20 Kohlenstoffatome, besonders bevorzugt 6 bis 15 Kohlenstoffatome, auf. Entsprechende aliphatische monomere Isocyanate können beispielsweise ausgewählt werden aus der Gruppe, bestehend aus Isophorondiisocyanat, 1,4-Cyclohexyldiisocyanat, 1,1 -Methylen-bis-(4-isocyanatocyclohexan), 1,2-Bis-(4-isocyanatononyl)-3-heptyl-4-pentyl-cyclohexan und Hexamethylen-1,6-diisocyanat. Hierbei ist die Verwendung von Isophorondiisocyanat und Hexamethylen-1,6-diisocyanat bevorzugt.The aliphatic isocyanates have as R preferably 6 to 20 carbon atoms, more preferably 6 to 15 carbon atoms. Corresponding aliphatic monomeric isocyanates may for example be selected from the group consisting of isophorone diisocyanate, 1,4-cyclohexyl diisocyanate, 1,1-methylene-bis (4-isocyanatocyclohexane), 1,2-bis (4-isocyanatononyl) -3- heptyl-4-pentylcyclohexane and hexamethylene-1,6-diisocyanate. Here, the use of isophorone diisocyanate and hexamethylene-1,6-diisocyanate is preferred.

Die vorgenannten Verbindungen sind handelsüblich und sind beispielsweise bei der Firma Rhein Chemie Rheinau GmbH oder die der Bayer MaterialScience AG erhältlich.The abovementioned compounds are commercially available and are obtainable, for example, from Rhein Chemie Rheinau GmbH or Bayer MaterialScience AG.

Allophanate im Sinne der Erfindung sind vorzugsweise Verbindungen der Formel (VI)

Figure imgb0008
wobei R' und R" unabhängig voneinander ein Alkylrest mit 1 bis 20 Kohlenstoffatomen oder ein Arylrest mit 6 bis 20 Kohlenstoffatomen ist,
und R'" die Bedeutung eines Alkylrestes mit 1 bis 20 Kohlenstoffatomen hatAllophanates within the meaning of the invention are preferably compounds of the formula (VI)
Figure imgb0008
where R 'and R "independently of one another are an alkyl radical having 1 to 20 carbon atoms or an aryl radical having 6 to 20 carbon atoms,
and R '"has the meaning of an alkyl radical having 1 to 20 carbon atoms

Diese Verbindungen sind im Allgemeinen durch Umsetzung beliebiger urethan- und/oder harnstoffgruppenhaltiger Ausgangsverbindungen, enthaltend Einheiten der allgemeinen Formel (R"OOC-NHR'), mit Monoisocyanaten der allgemeinen Formel R"'-NCO oder mit Diisocyanaten der allgemeinen Formel OCN-A-NCO zugänglich, wobei R'" bzw. A bevorzugt ein Alkylrest mit 1 bis 20 Kohlenstoffatomen oder ein Arylrest mit 6 bis 20 Kohlenstoffatomen ist und R' und R" unabhängig voneinander für Alkylreste mit 1 bis 20 Kohlenstoffatomen oder Arylreste mit 6 bis 20 Kohlenstoffatomen stehen.These compounds are generally obtained by reacting any urethane and / or urea group-containing starting compounds containing units of the general formula (R "OOC-NHR '), with monoisocyanates of the general formula R"' - NCO or with diisocyanates general formula OCN-A-NCO accessible, wherein R '"or A is preferably an alkyl radical having 1 to 20 carbon atoms or an aryl radical having 6 to 20 carbon atoms and R' and R" are independently alkyl radicals having 1 to 20 carbon atoms or aryl radicals with 6 to 20 carbon atoms.

Als Monoisocyanate eignen sich beliebige aromatische, aliphatische und cycloaliphatische Monoisocyanate mit bis zu 20 Kohlenstoffatomen, wie Methylisocyanat, Isopropylisocyanat, n-Butylisocyanat, n-Hexylisocyanat, Cyclohexylisocyanat, Stearylisocyanat, die gegebenenfalls halogenierten Phenylisocyanate, 1-Naphtylisocyanat, die gegebenenfalls chlorierten oder fluorierten m-, o-, und p-Toloylisocyanate, p-Isopropylphenylisocyanat, 2,6-Diisopropyl-phenylisocyanat und p-Toluolsulfonyldiisocyanat.Suitable monoisocyanates are any aromatic, aliphatic and cycloaliphatic monoisocyanates containing up to 20 carbon atoms, such as methyl isocyanate, isopropyl isocyanate, n-butyl isocyanate, n-hexyl isocyanate, cyclohexyl isocyanate, stearyl isocyanate, the optionally halogenated phenyl isocyanates, 1-naphthyl isocyanate, which may be chlorinated or fluorinated. , o-, and p-tooleyl isocyanates, p-isopropylphenyl isocyanate, 2,6-diisopropylphenyl isocyanate and p-toluenesulfonyl diisocyanate.

Als Diisocyanate eignen sich beliebige aromatische, aliphatische und cycloaliphatische Diisocyanate mit 6 bis 40 Kohlenstoffatomen, vorzugsweise 6 bis 15 Kohlenstoffatomen, wie besonders bevorzugt Isophorondiisocyanat, 1,4-Cyclohexyldiisocyanat, 1,1-Methylen-bis-(isocyanatohexan), 1,2-Bis-(4-Isocyanatononyl)-3-heptyl-4-pentylcyclohexan, Hexamethylen-1,6-diisocyanat, 2,4-Diisocyanatotoluol, 2,6-Diisocyanatotoluol, 1,5-Naphthylendiisocyanat, 4,4'-Methylen-diphenyldiisocyanat, 1,3-Bis-(3-isocyanto-4-methylphenyl)-2,4-dioxodiazetidin, N,N'-Bis-(4-methyl-3-isocyanatophenyl)-Harnstoff und Tetramethylxylylendiisocyanat. Bevorzugt hiervon ist Hexamethylen-1,6-diisocyanat.Suitable diisocyanates are any aromatic, aliphatic and cycloaliphatic diisocyanates having 6 to 40 carbon atoms, preferably 6 to 15 carbon atoms, more preferably isophorone diisocyanate, 1,4-cyclohexyl diisocyanate, 1,1-methylene-bis- (isocyanatohexane), 1,2- Bis (4-isocyanatononyl) -3-heptyl-4-pentylcyclohexane, hexamethylene-1,6-diisocyanate, 2,4-diisocyanatotoluene, 2,6-diisocyanatotoluene, 1,5-naphthylene diisocyanate, 4,4'-methylene diphenyl diisocyanate , 1,3-bis (3-isocyanto-4-methylphenyl) -2,4-dioxodiazetidine, N, N'-bis (4-methyl-3-isocyanatophenyl) urea and tetramethylxylylene diisocyanate. Preferred of these is hexamethylene-1,6-diisocyanate.

Die im Rahmen der vorliegenden Erfindung besonders bevorzugten Allophanate sind Verbindungen der Formel (VII)

Figure imgb0009
wobei R4 und R6 innerhalb des Moleküls gleich oder verschieden sein können und C1-C6-Alkyl, vorzugsweise -(CH2)6- bedeuten, und R5 C1-C6-Alkyl entspricht.The allophanates which are particularly preferred in the context of the present invention are compounds of the formula (VII)
Figure imgb0009
wherein R 4 and R 6 may be the same or different within the molecule and C 1 -C 6 alkyl, preferably - (CH 2 ) 6 -, and R 5 is C 1 -C 6 alkyl.

Entsprechende Allophanate sowie deren Herstellung sind beispielsweise in der EP 0 000 194A beschrieben, dessen diesbezügliche Offenbarung in die vorliegende Erfindung unter Bezugnahme eingeschlossen wird. Die vorgenannten Verbindungen sind handelsüblich und sind beispielsweise bei der Firma Bayer MaterialScience AG erhältlich.Corresponding allophanates and their preparation are for example in the EP 0 000 194A whose disclosure in the present invention is incorporated by reference. The abovementioned compounds are commercially available and are obtainable, for example, from Bayer MaterialScience AG.

Carbodiimide im Sinne der Erfindung sind vorzugsweise Verbindungen der Formel (VIII)

        R11-(-N=C=N-R12-)m-R13     (VIII),

in der

  • m einer ganzen Zahl von 1 bis 500 entspricht,
  • R12 für C1-C18-Alkylen, C5-C18-Cycloalkylen-, Arylen und/oder C7-C18- Aralkylen steht
  • R11 für R12-NCO, R12-NHCONHR9, R12-NHCONR9R7 oder R12-NHCOOR8 steht und
  • R13 steht -NCO, -NHCONHR9, -NHCONR9R7 oder -NHCOOR8 steht,
  • wobei in R11 unabhängig voneinander R9 und R7 gleich oder verschieden sind und einen C1-C6-Alkyl-, C6-C10-Cycloalkyl- oder C7-C18-Aralkylrest darstellen und R8 eine der Bedeutungen von R11 hat oder einen Polyester- oder Polyamidrest oder -(CH2)h-O-[(CH2)k-O]g-R10 entspricht,
  • mit h = 1-3, k= 1-3, g = 0-12, wobei
  • R10 die Bedeutung von H oder C1-C4-Alkyl hat.
Carbodiimides in the context of the invention are preferably compounds of the formula (VIII)

R 11 - (- N = C = NR 12 ) m -R 13 (VIII),

in the
  • m is an integer from 1 to 500,
  • R 12 is C 1 -C 18 alkylene, C 5 -C 18 cycloalkylene, arylene and / or C 7 -C 18 aralkylene
  • R 11 is R 12 -NCO, R 12 is -NHCONHR 9 , R 12 is -NHCONR 9 R 7 or R 12 is -NHCOOR 8 and
  • R 13 is -NCO, -NHCONHR 9 , -NHCONR 9 R 7 or -NHCOOR 8 ,
  • where in R 11 independently of one another R 9 and R 7 are identical or different and represent a C 1 -C 6 -alkyl, C 6 -C 10 -cycloalkyl or C 7 -C 18 -aralkyl radical and R 8 has one of the meanings of R 11 has or is a polyester or polyamide radical or - (CH 2 ) h -O - [(CH 2 ) k -O] g -R 10 ,
  • with h = 1-3, k = 1-3, g = 0-12, where
  • R 10 has the meaning of H or C 1 -C 4 alkyl.

Ebenfalls einsetzbar sind auch Gemische von Carbodiimiden der Formel (VIII), inklusive der entsprechenden Oligomere und/oder Polymere, wobei polymere Carbodiimide bevorzugt sind.Also suitable are mixtures of carbodiimides of the formula (VIII), including the corresponding oligomers and / or polymers, with polymeric carbodiimides being preferred.

Die Verbindungen nach Formel (VIII) sind kommerziell erhältlich, z.B. bei der Firma Rhein Chemie Rheinau GmbH oder lassen sich nach den dem Fachmann geläufigen Verfahren herstellen, wie z.B. beschrieben in DE-A-11 30 594 oder US-A 2 840 589 oder durch die Kondensation von Diisocyanaten unter Abspaltung von Kohlendioxid bei erhöhten Temperaturen, z.B. bei 40 °C bis 200 °C, in Gegenwart von Katalysatoren. Als Katalysatoren haben sich vorzugsweise starke Basen oder Phosphorverbindungen bewährt. Bevorzugt werden Phospholenoxide, Phospholidine oder Phospholinoxide sowie die entsprechenden Sulfide verwendet. Ferner können als Katalysatoren tertiäre Amine, basisch reagierende Metallverbindungen, Carbonsäuremetallsalze und nicht basische Organometallverbindungen verwendet werden.The compounds of the formula (VIII) are commercially available, for example from Rhein Chemie Rheinau GmbH, or can be prepared by the processes familiar to the person skilled in the art, as described, for example, in US Pat DE-A-11 30 594 or US-A 2,840,589 or by the condensation of diisocyanates with elimination of carbon dioxide at elevated temperatures, for example at 40 ° C to 200 ° C, in the presence of catalysts. As catalysts preferably strong bases or phosphorus compounds have proven. Preference is given to using phospholene oxides, phospholidines or phospholine oxides and the corresponding sulfides. Further, as catalysts, tertiary amines, basic metal compounds, carboxylic acid metal salts and non-basic organometallic compounds can be used.

Die vorgenannten Verbindungen sind handelsüblich und sind beispielsweise bei der Firma Rhein Chemie Rheinau GmbH erhältlich.The abovementioned compounds are commercially available and are obtainable, for example, from Rhein Chemie Rheinau GmbH.

Geblockte Aktivatoren, vorzugsweise mit Lactamen, besonders bevorzugt Caprolactam, oder mit Phenolen, Oximen und/oder Epoxiden geblockte Aktivatoren sind beispielsweise herstellbar über die Umsetzung mindestens einer Verbindung der Formeln (I) bis (VIII) mit mindestens einem Lactam, Caprolactam, Phenol, Oxim und/oder Epoxid bei Temperaturen von 80 bis 100°C nach den, dem Fachmann geläufigen Verfahren.Blocked activators, preferably with lactams, particularly preferably caprolactam, or activators blocked with phenols, oximes and / or epoxides can be prepared, for example, by reacting at least one compound of the formulas (I) to (VIII) with at least one lactam, Caprolactam, phenol, oxime and / or epoxide at temperatures of 80 to 100 ° C according to the methods known in the art.

Zur Herstellung der Gusspolyamide werden in einer Ausführungsform der Erfindung, bezogen auf Lactam, vorzugsweise folgende Anteile eingesetzt:
0,1 bis 3 Gew.%, bevorzugt 0,2 bis 1,5 Gew.% der erfindungsgemäßen Zusammensetzung und 0,1 bis 2 Gew.%, bevorzugt 0,5 bis 1 Gew.% an Aktivator.
For the preparation of the cast polyamides, the following proportions are preferably used in one embodiment of the invention, based on lactam:
0.1 to 3 wt.%, Preferably 0.2 to 1.5 wt.% Of the inventive composition and 0.1 to 2 wt.%, Preferably 0.5 to 1 wt.% Of activator.

In einer bevorzugten Ausführungsform der Erfindung ist das Gusspolyamid erhältlich durch die Polymerisation von Lactam, vorzugsweise Caprolactam, mit
0,1 bis 3 Gew.% der erfindungsgemäßen Zusammensetzung enthaltend Natriumlactamat a) als vorzugsweise 18-20 Gew.%ige Caprolactam-Lösung mit 0,1 bis 5 Gew.%, bevorzugt, 0,5 - 4 Gew.%, besonders bevorzugt 1,5 - 2,5 Gew.% Na-Aminocapronat und
0,1 bis 2 Gew.% mindestens eines Vertreters, ausgewählt aus der Gruppe Hexamethylen-1,6-diisocyanat, mit Caprolactam geblocktem Hexamethylen-1,6-diisocyanat, Biuret der Formel (V) mit p = 6 und/oder einem Uretdion aus Basis von 2,4-Diisocyanatotoluol als Aktivator.
In a preferred embodiment of the invention, the cast polyamide is obtainable by the polymerization of lactam, preferably caprolactam
0.1 to 3 wt.% Of the inventive composition containing sodium lactamate a) as preferably 18-20 wt.% Caprolactam solution with 0.1 to 5 wt.%, Preferably, 0.5 to 4 wt.%, Particularly preferably 1.5-2.5% by weight of Na-aminocapronate and
0.1 to 2% by weight of at least one representative selected from the group of hexamethylene-1,6-diisocyanate, caprolactam-blocked hexamethylene-1,6-diisocyanate, biuret of the formula (V) with p = 6 and / or a uretdione based on 2,4-diisocyanatotoluene as activator.

In einer weiteren bevorzugten Ausführungsform der Erfindung enthält die Mischung zur Herstellung von Gusspolyamiden zusätzlich mindestens einen weiteren Zusatz- und Hilfsstoff, ausgewählt aus Füll- und/oder Verstärkungsstoffen, Polymeren und/oder weiteren Zusatzstoffen.In a further preferred embodiment of the invention, the mixture for the production of cast polyamides additionally contains at least one further additive and adjuvant, selected from fillers and / or reinforcing materials, polymers and / or further additives.

Füll- und/oder Verstärkungsstoff im Sinne der Erfindung sind organische oder anorganische Füll- und/oder Verstärkungsstoffe. Bevorzugt sind anorganische Füllstoffe, insbesondere Kaolin, Kreide, Wollastonit, Talkum, Calciumcarbonat, Silikate, Titandioxid, Zinkoxid, Graphit, Graphene, Glaspartikel (z.B. Glaskugeln), nanoskalige Füllstoffe, (wie Kohlenstoff-Nanoröhren carbonanotubes), carbon black, Schichtsilikate, nanoskalige Schichtsilikate, nanoskaliges Aluminiumoxid (Al2O3), nanoskaliges Titandioxid (TiO2) und/oder nanoskaliges Siliciumdioxid (SiO2).Fillers and / or reinforcing agents in the context of the invention are organic or inorganic fillers and / or reinforcing materials. Preference is given to inorganic fillers, in particular kaolin, chalk, wollastonite, talc, calcium carbonate, silicates, titanium dioxide, zinc oxide, graphite, graphenes, glass particles (eg glass spheres), nanoscale fillers (such as carbon nanotubes carbonanotubes), carbon black, phyllosilicates, nanoscale phyllosilicates , nanoscale alumina (Al 2 O 3 ), nanoscale titania (TiO 2 ), and / or nanoscale silica (SiO 2 ).

Weiterhin bevorzugt ist der Einsatz von Faserstoffen als Füll- und/oder Verstärkungsstoff. Die Füll- und/oder Verstärkungsstoffe werden in der Regel ausgewählt aus der Gruppe umfassend Mineralien in für Thermoplastanwendungen üblicher Korngröße, insbesondere Kaolin, Kreide, Wollastonit oder Talkum, Kohlenstoff- oder Glasfasern, vorzugsweise gemahlene Glasfasern, besonders bevorzugt Glas- und Kohlenstofffasern.Further preferred is the use of fibers as filling and / or reinforcing material. The fillers and / or reinforcing materials are usually selected from the group comprising minerals in customary for thermoplastic applications grain size, in particular kaolin, chalk, wollastonite or talc, carbon or glass fibers, preferably ground glass fibers, particularly preferably glass and carbon fibers.

Besonders bevorzugt kommen ein oder mehrere Faserstoffe zum Einsatz, ausgewählt aus bekannten anorganischen Verstärkungsfasern, insbesondere Borfasern, Glasfasern, Kohlenstofffasern, Kieselsäurefasern, Keramikfasern und Basaltfasern; organischen Verstärkungsfasern, insbesondere Aramidfasern, Polyesterfasern, Nylonfasern, Polyethylenfasern; und Naturfasern, insbesondere Holzfasern, Flachsfasern, Hanffasern und Sisalfasern. Insbesondere bevorzugt ist der Einsatz von Glasfasern, insbesondere Schnittglasfasern, Kohlenstofffasern, Aramidfasern, Borfasern, Metallfasern und/oder Kaliumtitanatfasem.Particular preference is given to using one or more fibrous materials selected from known inorganic reinforcing fibers, in particular boron fibers, glass fibers, carbon fibers, silica fibers, ceramic fibers and basalt fibers; organic reinforcing fibers, especially aramid fibers, polyester fibers, nylon fibers, polyethylene fibers; and natural fibers, especially wood fibers, flax fibers, hemp fibers and sisal fibers. Particularly preferred is the use of glass fibers, in particular chopped glass fibers, carbon fibers, aramid fibers, boron fibers, metal fibers and / or potassium titanate fibers.

Insbesondere können auch Mischungen der genannten Füll- und/oder Verstärkungsstoffe eingesetzt werden. Besonders bevorzugt werden als Füll- und/oder Verstärkungsstoffe Glasfasern und/oder Glaspartikel, insbesondere Glaskugeln, ausgewählt.In particular, it is also possible to use mixtures of the stated fillers and / or reinforcing materials. Glass fibers and / or glass particles, in particular glass beads, are particularly preferably selected as fillers and / or reinforcing materials.

Die Menge an einzusetzenden Füll- und/oder Verstärkungsstoffen beträgt vorzugsweise 30 bis 90 Gew.-%, insbesondere von 30-80 Gew.-%, bevorzugt 30 bis 50 Gew.-%, weiterhin bevorzugt von 50 bis 90 Gew.-%.The amount of fillers and / or reinforcing substances to be used is preferably from 30 to 90% by weight, in particular from 30 to 80% by weight, preferably from 30 to 50% by weight, more preferably from 50 to 90% by weight.

Polymere im Sinne der Erfindung sind: Polystyrol, Styrol-Copolymersiate, insbesondere Styrol-Acrylnitril-Copolymere (SAN), Acrylnitril-Butadien-Styrol-Copolymere (ABS) oder StyrolButadien-Copolymere (SB), Polyphenylenoxidether, Polyolefine, insbesondere Polyethylen (HTPE (high-temperature-polyethylene), LTPE (low-temperature-polyethylene), Polypropylen oder Polybuten-1, Polytetrafluorethylen, Polyester, insbesondere Polyethylenterephthalat (PET); Polyamide, Polyether, insbesondere Polyethylenglykol (PEG), Polypropylenglykol oder Polyethersulfone (PESU oder PES); Polymere aus Vinylgruppen enthalten Monomeren, insbesondere Polyvinylchlorid, Polyvinylidenchloride, Polystryrol, schlagzäh-modifiziertes Polystyrol, Polyvinylcarbazol, Polyvinylacetat oder Polyvinylalkohol, Polyisobutylene Polybutadien und/oder Polysulfone. Es ist weiterhin die Verwendung von Copolymeren als Polymer möglich, die aus den Monomereinheiten der oben genannten Polymere bestehen.Polymers in the context of the invention are: polystyrene, styrene copolymers, in particular styrene-acrylonitrile copolymers (SAN), acrylonitrile-butadiene-styrene copolymers (ABS) or styrene-butadiene copolymers (SB), polyphenylene oxide ethers, polyolefins, in particular polyethylene (HTPE ( high-temperature polyethylene), LTPE (low-temperature polyethylene), polypropylene or polybutene-1, polytetrafluoroethylene, polyesters, in particular polyethylene terephthalate (PET), polyamides, polyethers, in particular polyethylene glycol (PEG), polypropylene glycol or polyethersulfones (PESU or PES) Polymers made from vinyl groups contain monomers, in particular polyvinyl chloride, polyvinylidene chlorides, polystyrene, impact-modified polystyrene, polyvinylcarbazole, polyvinyl acetate or polyvinyl alcohol, polyisobutylenes polybutadiene and / or polysulfones Furthermore, the use of copolymers as polymer consisting of the monomer units of the above-mentioned Polymers exist.

In einer weiteren Ausführungsform der Erfindung kann das einzusetzende Polymer Gruppen enthalten, die zur Bildung von Block- und/oder Pfropf-Copolymeren mit dem aus den Monomeren gebildeten Polymeren, geeignet sind. Beispiele für solche Gruppen sind Epoxy-, Amin-, Carboxyl-Anhydrid-, Oxazolin-, Carbodiimid-, Urethan-, Isocyanat- und Lactam-Gruppen. Polymere mit Carbodiimid-Gruppen werden dann eingesetzt, wenn kein Carbodiimid als Aktivator eingesetzt wird.In a further embodiment of the invention, the polymer to be used may contain groups which are suitable for forming block and / or graft copolymers with the polymer formed from the monomers. Examples of such groups are epoxy, amine, carboxyl anhydride, oxazoline, carbodiimide, urethane, isocyanate and lactam groups. Polymers with carbodiimide groups are used when no carbodiimide is used as activator.

Optional enthaltene Polymer ist vorzugsweise in einer Menge von 0 bis 40 Gew.-%, bevorzugt von 0 bis 20 Gew.-%, besonders bevorzugt in einer Menge von 0 bis 10 Gew.-% enthalten.Optionally contained polymer is preferably contained in an amount of 0 to 40 wt .-%, preferably from 0 to 20 wt .-%, particularly preferably in an amount of 0 to 10 wt .-%.

In einer bevorzugten Ausführungsform enthält erfindungsgemäße Zusammensetzung weitere Zusatzstoffe. Bevorzugt werden die Zusatzstoffe in einer Menge von 0 bis 5 Gew.-%, besonders bevorzugt von 0 bis 4 Gew.-%, ganz besonders bevorzugt von 0 bis 3,5 Gew.-% eingesetzt. Als Zusatzstoffe können bevorzugt Stabilisatoren, insbesondere Kupfersalze, Farbstoffe, Antistatika, Füllöle, Stabilisatoren, Oberflächenverbesserer, Sikkative, Entformungs-Hilfsmittel, Trennmittel, Antioxidantien, Lichtstabilisatoren, PVC-Stabilisatoren, Gleitmittel, Polyole, Flammschutzmittel, Treibmittel, Schlagzähmodifikatoren und/oder Nukleierungshilfsmittel zugesetzt werden.In a preferred embodiment, the composition according to the invention contains further additives. The additives are preferably used in an amount of from 0 to 5% by weight, particularly preferably from 0 to 4% by weight, very particularly preferably from 0 to 3.5% by weight. Stabilizers, in particular copper salts, dyes, antistatic agents, fillers, stabilizers, surface improvers, siccatives, mold release agents, release agents, antioxidants, light stabilizers, PVC stabilizers, lubricants, polyols, flame retardants, blowing agents, impact modifiers and / or nucleating agents may preferably be added as additives ,

Als Schlagzähmodifikatoren sind insbesondere Polydien-Polymere, vorzugsweise Polybutadien, Polyisopren, enthaltend Anhydrid und/oder Epoxigruppen geeignet. Das Polydien-Polymer weist eine Glasübergangstemperatur unter 0 °C, bevorzugt unter -10 °C, besonders bevorzugt unter -20°C auf. Das Polydien-Polymer kann auf der Basis eines Polydien-Copolymers mit Polyacrylaten, Polyethylenacrylaten und/oder Polysiloxanen basieren und mittels der gängigen Verfahren hergestellt werden, vorzugsweise durch Emulsionspolymerisation, Suspensions-polymerisation, Lösungspolymerisation, Gasphasenpolymerisation.Particularly suitable impact modifiers are polydiene polymers, preferably polybutadiene, polyisoprene, containing anhydride and / or epoxy groups. The polydiene polymer has a glass transition temperature below 0 ° C, preferably below -10 ° C, more preferably below -20 ° C. The polydiene polymer can be based on a polydiene copolymer with polyacrylates, polyethylene acrylates and / or polysiloxanes and prepared by the usual methods, preferably by emulsion polymerization, suspension polymerization, solution polymerization, gas phase polymerization.

In einer weitern bevorzugten Ausführungsform der Erfindung wird als Zusatzstoff Polyol eingesetzt, um die Schlagzähigkeit zu verbessern. Diese sind z.B. erhältlich von der Rhein Chemie Rheinau GmbH unter der Bezeichnung Addonyl® 8073. Ebenfalls einsetzbar sind Polyoltriamine geeignet, um die Tieftemperatur-Schlagzähigkeit zu verbessern. Ein geeignetes Produkt ist Addonyl® 8112. Vorzugsweise werden die Polyole im Konzentrationsbereich 1-20 Gew.-% eingesetzt.In a further preferred embodiment of the invention is used as an additive polyol to improve the impact resistance. These are e.g. available from Rhein Chemie Rheinau GmbH under the name Addonyl® 8073. Also usable are polyoltriamines suitable for improving the low-temperature impact strength. A suitable product is Addonyl® 8112. Preferably, the polyols are used in the concentration range 1-20 wt .-%.

Die optionale Zugabe von Füll- und/oder Verstärkungsstoffen und weiteren Zusatzstoffen kann vor oder zusammen mit der Zugabe von Katalysator und/oder Aktivator erfolgen.The optional addition of fillers and / or reinforcing materials and other additives can be carried out before or together with the addition of catalyst and / or activator.

In einer weiteren Ausführung der vorliegenden Erfindung kann die Polymerisation zur Herstellung von Gusspolyamiden nach einem geeigneten Formgebungsverfahren, vorzugsweise Spritzguss, Standgussverfahren, Rotationsgussverfahren, durchgeführt werden.In a further embodiment of the present invention, the polymerization for the production of cast polyamides may be carried out by a suitable molding process, preferably injection molding, casting, rotational molding.

Bei Spritzguss, Standgussverfahren, Rotationsgussverfahren handelt es sich um dem Fachmann geläufige Verfahren.Injection molding, stand casting, rotational molding process are familiar to those skilled in the process.

Der Rahmen der Erfindung erfasst alle oben stehenden und im Folgenden aufgeführten allgemeinen oder in Vorzugsbereichen genannten Restedefinitionen, Indizes, Parameter und Erläuterungen untereinander, also auch zwischen den jeweiligen Bereichen und Vorzugsbereichen in beliebiger Kombination.The scope of the invention covers all of the above-mentioned general or preferred radical definitions, indices, parameters and explanations with one another, ie also between the respective ranges and preferred ranges in any desired combination.

Ein weiterer Gegenstand der vorliegenden Erfindung ist die Verwendung der erfindungsgemäßen Zusammensetzung als Katalysator zur Herstellung von Gusspolyamid.Another object of the present invention is the use of the composition of the invention as a catalyst for the production of cast polyamide.

Darüber hinaus ist die Verwendung der erfindungsgemäßen der Zusammensetzung zur Herstellung von Rollen, vorzugsweise für Personenaufzüge und Halbzeuge, vorzugsweise Behälter, Zahnräder, Rohre, Stäbe und Platten für den Maschinenbau und die Automobilindustrie ein weiteren Gegenstand der Erfindung.In addition, the use of the composition according to the invention for the production of rolls, preferably for passenger lifts and semi-finished products, preferably containers, gears, tubes, rods and plates for mechanical engineering and the automotive industry is a further subject of the invention.

Die nachfolgenden Beispiele dienen der Erläuterung der Erfindung, ohne dabei limitierend zu wirken.The following examples serve to illustrate the invention without being limiting.

Ausführungsbeispiele:EXAMPLES Reagenzien:reagents:

Caprolactam trocken (EP > 69 °C) von der Firma Lanxess Deutschland GmbH
Aktivator, ein Hexamethylen-1,6-Diisocyanat (HDI)-Biuret, 70% in N-Ethylpyrrolidon, kommerziell erhältlich bei der Rhein Chemie Rheinau GmbH,
Erfindungsgemäße Zusammensetzung als Katalysator (A) mit ca. 18 % Natriumcaprolactamat und 2,0 % Natriumaminocapronat in Caprolactam.
Caprolactam dry (EP> 69 ° C) from the company Lanxess Germany GmbH
Activator, a hexamethylene-1,6-diisocyanate (HDI) biuret, 70% in N-ethylpyrrolidone, commercially available from Rhein Chemie Rheinau GmbH,
Inventive composition as catalyst (A) with about 18% sodium caprolactamate and 2.0% sodium aminocapronate in caprolactam.

Zusammensetzung nach dem Stand der Technik als Katalysator (B) mit ca. 18 % Natriumcaprolactamat in Caprolactam, Vergleich.Composition of the prior art as catalyst (B) with about 18% sodium caprolactamate in caprolactam, comparison.

Geräte:Equipment:

Die verwendete Apparatur zur Schmelzaufbereitung bestand aus:

  • 2 Dreihalskolben (500 ml) im Ölbad beheizt
  • 2 KPG-Rührer mit Hülse
  • 2 Gaskappen je 1 mit und 1 ohne Hahn
  • 1 Vakuumpumpe mit Kühlfalle und Manometer.
The apparatus used for melt processing consisted of:
  • 2 three-necked flasks (500 ml) heated in an oil bath
  • 2 KPG stirrer with sleeve
  • 2 gas caps each with 1 and 1 without tap
  • 1 vacuum pump with cold trap and pressure gauge.

Die verwendete Apparatur zur Temperaturmessung bestand aus:

  • Temperaturmessgerät Testo 175-T3 mit IR-Serial Interface
  • Thermodraht zum Verbleib in der ausgehärteten Probe
  • Becherglas 600 ml (hohe Form) und einer
  • Beheizung für das Becherglas (Metallblock, Ölbad).
The temperature measuring apparatus used consisted of:
  • Temperature measuring device Testo 175-T3 with IR-Serial Interface
  • Thermal wire to remain in the cured sample
  • Beaker 600 ml (high form) and one
  • Heating for the beaker (metal block, oil bath).

Durchführung und Messung der Topfzeit:Carrying out and measuring the pot life:

Kolben A wurde mit 196,8 g Caprolactam und 3,2 g Aktivator, Kolben B1/2 mit 192 g Caprolactam und 8 g Katalysator (A) bzw. (B) beschickt.Flask A was charged with 196.8 g of caprolactam and 3.2 g of activator, flask B1 / 2 with 192 g of caprolactam and 8 g of catalyst (A) and (B), respectively.

Die Schmelzen aus den Kolben A und Kolben B1/2 wurden bei 110 - 130 °C (± 2 °C) in einem Ölbad unter Vakuum (<15 mbar) 20 Minuten aufbereitet.The melts from flask A and flask B1 / 2 were conditioned at 110-130 ° C (± 2 ° C) in an oil bath under vacuum (<15 mbar) for 20 minutes.

Nach Belüften mit Stickstoff wurden Komponenten aus Kolben A und Kolben B in einen Dreihalskolben vereinigt, kurz durchgerührt und in das 600 ml Becherglas überführt.After venting with nitrogen, components from flask A and flask B were combined in a three-necked flask, stirred briefly and transferred to the 600 ml beaker.

Die Formtemperatur (Becherglas) betrug 160° C. Die Polymerisationszeit betrug in der Regel 10 - 20 Minuten.The mold temperature (beaker) was 160 ° C. The polymerization time was generally 10 to 20 minutes.

Die Trübungstest erfolgten im Trockenschrank 85 °C nach einem Zeitraum von 3 h. Die Beurteilung erfolgte visuell.The turbidity tests were carried out in a drying oven at 85 ° C. after a period of 3 hours. The assessment was done visually.

Die Beurteilung der Qualität der Gusspolyamide in Bezug auf Kristallinität und Homogenität erfolgte anhand von REM-Aufnahmen (Raster-Elektronen-Mikroskop). Katalysator in Kolben B1/2 Topfzeit Trübungstest Kristallinität/Homogenität (s) (85 °C, 3 h) Gusspolyamid Katalysator A (erf.) 380 blank hoch Katalysator B (V) 270 stark trüb gering Vergleichsbeispiel = vergl., Erfindungsgemäß = erf.The evaluation of the quality of the cast polyamides in terms of crystallinity and homogeneity was carried out on the basis of SEM images (scanning electron microscope). Catalyst in flask B1 / 2 pot life turbidity test Crystallinity / homogeneity (S) (85 ° C, 3 h) cast nylon Catalyst A (erf.) 380 bright high Catalyst B (V) 270 very cloudy low Comparative Example = Comp., Inventive = Comp.

Die Mischungen nach dem Stand der Technik weisen i.d.R. Topfzeiten von < 300s auf, was zu Inhomogenitäten und einer geringen Kristallinität des Gusspolyamids führt. Darüber hinaus polymerisieren die den Katalysator enthaltenden Schmelzen bereits in der Vorlage an und verstopfen so die der Gussform vorgeschalteten Filter.The blends of the prior art have i.d.R. Pot lives of <300s, resulting in inhomogeneities and a low crystallinity of the cast polyamide. In addition, the melts containing the catalyst polymerize already in the template and thus clog the filter upstream of the mold.

Die Beispiele zeigen, dass der erfindungsgemäße Katalysator Topfzeiten von deutlich über 300s aufweist. Die erfindungsgemäßen Zusammensetzungen trüben zudem nicht ein.The examples show that the catalyst according to the invention has pot lives of well over 300s. Moreover, the compositions according to the invention do not tarnish.

Dadurch können auch großvolumige qualitativ hochwertige Gusspolyamid-Teile hergestellt werden. Weiterhin kann die Qualität der so hergestellten Gusspolyamide bezüglich Kristallinität bzw. Homogenität deutlich verbessert werden.As a result, it is also possible to produce large-volume high-quality cast polyamide parts. Furthermore, the quality of the cast polyamides thus produced can be significantly improved with respect to crystallinity or homogeneity.

Claims (14)

  1. Composition comprising
    a) at least one lactamate and
    b) at least one salt of an organic acid substituted by heteroatoms and/or ester of an organic acid substituted by heteroatoms, and optionally
    c) a lactam or a mixture of two or more lactams.
  2. Composition according to Claim 1, characterized in that the lactamate is at least one compound selected from the group of the alkali metal aluminodilactamates and alkali metal and/or alkaline earth metal lactamates.
  3. Composition according to one or more of Claims 1 and 2, characterized in that the ester b) comprises alkyl esters, preferably methyl and/or ethyl esters.
  4. Composition according to one or more of Claims 1 and 2, characterized in that the salt of the organic acid b) substituted by heteroatoms, preferably by amino groups, has 1 to 12 carbon atoms, preferably 4 to 6 carbon atoms.
  5. Composition according to one or more of Claims 1 to 4, characterized in that the heteroatoms are nitrogen, sulfur, phosphorus, preferably nitrogen, and/or halides, preferably chlorine and/or bromine.
  6. Composition according to Claim 5, characterized in that the salt of an organic acid substituted by heteroatoms and/or ester of an organic acid b) substituted by heteroatoms comprises aminocapronates and/or aminolaurates, preferably alkali metal and/or alkaline earth metal aminocapronates and/or -laurates, more preferably sodium aminocapronate, potassium aminocapronate and/or magnesium aminocapronate.
  7. Composition according to one or more of Claims 1 to 6, characterized in that the lactam corresponds to the general formula
    Figure imgb0011
    where R* is an alkylene group having 3 to 13 carbon atoms.
  8. Composition according to one or more of Claims 1 to 7, characterized in that constituents a) and b) are present in a ratio of 3:1 to 50:1, preferably 5:1 to 40:1, more preferably 9:1, and the proportion of lactam c), based on constituents a) and b), is preferably 0-99% by weight, more preferably 50-85% by weight.
  9. Process for preparing composition according to one or more of Claims 1 to 8, characterized in that the lactamate a) is prepared by reaction of at least one lactam which corresponds to or else may be different than lactam c) with alkali metal or alkaline earth metal alkoxides in the presence of at least one salt of an organic acid substituted by heteroatoms and/or ester of an organic acid b) substituted by heteroatoms with subsequent or simultaneous removal of the alcohol formed by distillation, and then further lactam c) is optionally added.
  10. Process for preparing composition according to Claim 9, characterized in that the salts of an organic acid substituted by heteroatoms and/or esters of the organic acids substituted by heteroatoms are prepared in situ by addition of acids, water and/or alkali metal and/or alkaline earth metal hydroxides to a) and optionally c).
  11. Cast polyamides obtainable by the polymerization of lactams with at least one composition of Claims 1 to 8 at temperatures of 80-180°C, optionally in the presence of activators and/or further additives and assistants.
  12. Process for producing cast polyamides obtainable by the polymerization of lactams with at least one composition of Claims 1 to 8 at temperatures of 80-120°C, preferably 120-160°C, in the presence of activators and optionally further additives and assistants.
  13. Use of the composition according to one or more of Claims 1 to 8 as a catalyst for the production of cast polyamide.
  14. Use of the composition according to one or more of Claims 1 to 8 for production of rollers, preferably for passenger elevators and semifinished products, for vessels, gears, tubes, bars and sheets for mechanical engineering and the automobile industry.
EP13727879.2A 2012-07-06 2013-06-06 Catalysts for the production of cast polyamide, method for producing and using same Active EP2870191B1 (en)

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JP6277575B1 (en) * 2017-07-03 2018-02-14 株式会社二幸技研 Nylon production method and molded nylon by alkali polymerization method
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